Polyurethane adhesive for a surface treatment-free fiber reinforced plastic

Description

[0001] The present invention relates to a two-component type polyurethane adhesive composition containing a high equivalent ratio of free NCO groups in the pre-polymer component to OH groups in the curative component. The urethane adhesive is applied directly to non-treated surfaces such as fiberglass rein forced plastics or metals.

[0002] In order to achieve satisfactory adhesion to fiberglass reinforced plastics (FRP) or between a FRP surface and a metal surface, it has conventionally been necessary to treat the surface of the fiberglass reinforced plastic before applying the polyurethane adhesive. Such surface treatments include mechanical treatments such as abrading or sanding the fiberglass reinforced plastic or metal surface, solvent treatments such as scrubbing the surface with a solvent such as methylene chloride, and chemical treatments such as applying a primer.

[0003] The prior art US-A-4552934/EP-A-63534, which serves as basis for the two-part form of the present claims, describes two-component polyurethane adhesives in which the curative component contains polyol partially pre-reacted with polyisocyanate, and also a polyamine such as ethylene diamine to inhibit sag.

[0004] EP-A-304083, which is in Article 54(3) EPC relationship with the present disclosure, describes two-component polyurethane adhesives for application to unprimed FRP parts. One component contains a blend of a urethane prepolymer and aliphatic isocyanate. The other (curative) component comprises a polyfunctional polyether polyol and optionally, inter alia, a diamine anti-sag agent.

[0005] Other relevant background disclosures may be found in US-A-3647513, US-A-3703426, US-A-3838093, US-A-3962498, US-A-4004050, US-A-4397707, US-A-3714127, US-A-3886122, US-A-3935051, US-A-4247676, US-A-4336298, US-A-4373082, US-A-4390678, US-A-4444976, US-A-4595445, US-A-4624996 and the article "New Urethane Adhesives and Adhesive Sealants for Bonding SMC" by Foreman et al, 34th Annual Technical Conference 1980, Reinforced Plastics/Composites Institute, The Society of the Plastics Industries, Inc.

[0006] The present invention seeks to provide novel two-component urethane adhesive systems which can be used for "treatment-free" adhesion of FRP.

[0007] In one aspect, the invention provides a two-component urethane adhesive, having

(a) a urethane prepolymer component, made from polyol intermediate and polyisocyanate with the polyisocyanate at equivalent ratio of at least 2 to give free NCO groups in the prepolymer component, and

(b) a curative component comprising curative polyol and primary polyamine,

   the urethane prepolymer component and the curative component being reactive together to form a crosslinked polyurethane;
characterised in that
   the relative amounts of components (a) and (b) are such that the equivalent ratio [NCO:(OH+NH₂)] of free prepolymer NCO groups in the prepolymer component to the polyol OH and primary polyamine NH₂ in the curative component is from 1.2 to 2.0.

[0008] In another aspect the invention relates to a process comprising adhering articles together, particularly FRP articles, using such a two-component urethane adhesive, and particularly in which one or both adhered surfaces are pretreatment-free for the adhesion.

[0009] In another aspect the invention relates to adhered composites obtained by such a process.

[0010] The two component polyurethane adhesive composition of the present invention contains a urethane prepolymer component and a curative component. The urethane prepolymer component is made from a polyol intermediate and an equivalent excess of a polyisocyanate so that free NCO groups exist. Such free NCO groups are located on the ends of the prepolymer and on the unreacted polyisocyanate. Typically, the prepolymer reaction takes place in the presence of a moisture free powdery mineral filler.

[0011] The polyol intermediate is generally a liquid polyether polyol or a polyester polyol, or combinations thereof having a number average molecular weight of from about 400 to about 10,000 with from about 2,000 to about 4,000 being preferred. A wide range of polyether or polyester polyols can be used in making the adhesives of the present invention such as diols, triols, tetrols. Polyether polyols are generally made by reacting an alkylene oxide having from 2 to 10 carbon atoms such as propylene oxide with a strong base such as potassium hydroxide, preferably in the presence of water or glycols. Polyethers having a highly branched chain are readily prepared from alkylene oxides and initiators having an active hydrogen functionality greater than 2. The higher functional initiators that are useful with the alkylene oxides described above include polyols, polyamines and amino alcohols having a total of three or more reactive hydrogen atoms on hydroxyl and primary or secondary amino groups and generally having up to 12 carbon atoms.

[0012] Suitable polyols include triols, such as glycerol, trimethylolpropane, butanetriols, hexanetriols, trialkanolamines, various diethylenetriamines, such as erythritol and pentaerythritol; pentols, hexols, such as dipentaerythritol and sorbitol; as well as alkyl glucosides, carbohydrates, polyhydroxy fatty acid esters such as caster oil; and polyoxy alkylated derivatives or polyfunctional compounds having three or more reactive hydrogen atoms, such as, the reaction product of trimethylolpropane, glycerol and other polyols with ethylene oxide, propylene oxide or other epoxides or copolymers thereof, e.g., copolymers of ethylene and propylene oxides, with ethylene oxide being used in a molar amount of not over 20 mol percent as compared to other alkylene oxides like propylene oxide. Examples of higher functional amino alcohols and polyamines include ethanolamine, diethanolamine, triethanolamine, isopropanolamine, diisopropanolamine, triisopropanolamine, 2-(2-aminoethylamino)ethanol, 2-amino-2(hydroxymethyl)-1,3-propanediol. ethylenediamine, diethylenetriamine, triethylenetetramine, and urea as well as various aryl polyamines such as 4,4',4''-methylidynetrianiline.

[0013] Other polyethers which can be utilized are those which are produced as by polymerization of tetrahydrofuran or epoxides (such as ethylene oxide, propylene oxide, butylene oxide, styrene oxide, or epichlorohydrin), or by addition of epoxide compounds (preferably ethylene oxide or propylene oxide), alone, in a mixture, or in succession, to starting components with reactive hydrogen atoms such as water, polyhydric alcohols, ammonia or polyfunctional amines.

[0014] Polyester polyols are formed from the condensation of one or more polyhydric alcohols having from 2 to 15 carbon atoms with one or more polycarboxylic acids having from 2 to 14 carbon atoms. Examples of suitable polyhydric alcohols include the following: ethylene glycol, propylene glycol such as 1,2-propylene glycol and 1,3-propylene glycol, glycerol; pentaerythritol; trimethylolpropane; 1,4,6-octanetriol; butanediol; pentanediol; hexanediol; dodecanediol; octanediol; chloropentanediol, glycerol monallyl ether; glycerol monoethyl ether, diethylene glycol; 2-ethylhexanediol-1,4; cyclohexanediol-1,4; 1,2,6-hexanetriol; 1,3,5-hexanetriol; 1,3-bis-(2-hydroxyethoxy)propane. Examples of polycarboxylic acids include the following: phthalic acid; isophthalic acid; terephthalic acid; tetrachlorophthalic acid; maleic acid; dodecylmaleic acid; octadecenylmaleic acid; fumaric acid; aconitic acid; trimellitic acid; tricarballylic acid; 3,3′-thiodipropionic acid; succinic acid; adipic acid; malonic acid, glutaric acid, pimelic acid, sebacic acid, cyclohexane-1,2-dicarboxylic acid; 1,4-cyclohexadiene-1,2-dicarboxylic acid; 3-methyl-3,5-cyclohexadiene-1,2-dicarboxylic acid and the corresponding acid anhydrides, acid chlorides and acid esters such as phthalic anhydride, phthaloyl chloride and the dimethyl ester of phthalic acid. Preferred polycarboxylic acids are the aliphatic and cycloaliphatic dicarboxylic acids containing no more than 14 carbon atoms and the aromatic dicarboxylic acids containing no more than 14 atoms. Any polyhydric alcohol having more than 2 hydroxyl groups or any polycarboxylic acid having more than 2 carboxylic groups used to make the polyesters should be used in only very minor amounts to prevent crosslinking and gelling.

[0015] Polyesters from lactones (for example ε-caprolactone) and polyacetals, polycarbonates or polybutadienes containing terminal hydroxyl groups are also suitable.

[0016] Highly preferred polyol intermediates include polypropylene ether diol, poly-1,2-butylene ether diol, poly-1,4-tetramethylene ether, and epsilon-polycaprolactone diols.

[0017] In order to achieve specific properties which are influenced by the composition and content of polyurethane hard blocks, small amounts of polyhydric alcohols are optionally utilized in combination with the above-noted liquid polyether or polyester polyol intermediates. The polyhydric alcohols generally have from 2 to 15 carbon atoms with specific examples including ethylene glycol, 1,2-propylene glycol, 1,3-propylene glycol, 1,4-butane diol, 2,3-butane diol, 1,5-pentanediol, glycerol, sorbitol, pentaerythritol, dipropylene glycol, diethylene glycol. The amount of such polyhydric alcohols is generally from about 0 or 1 to about 40 parts by weight and preferably from about 0 or 1 to about 10 parts by weight based upon 100 parts by weight of the polyether polyol intermediate, the polyester polyol intermediate, or combinations thereof.

[0018] The equivalent ratio of the polyisocyanate utilized to make the prepolymer to the hydroxyl containing polyol intermediate (NCO/OH) is generally from about 2 to about 20 and preferably from about 5 to about 10. Such large excesses are necessary to achieve relatively low molecular weight polyurethane prepolymers, since the hydroxyl groups of the intermediate are capped without significant chain extension. The polyisocyanates generally have the formula R(NCO)_n where n is an integer of 2, 3 or 4 with approximately 2 being preferred. However, it is to be understood that since combinations of various polyisocyanates can be utilized, the equivalent amount of isocyanate can vary and often is not an integer. R is an aliphatic having from 2 to 20 carbon atoms with from 6 to 15 carbon atoms being preferred, an aromatic including an alkyl substituted aromatic having from 6 to 20 carbon atoms with from 6 to 15 carbon atoms being preferred, or combinations thereof. Aromatic diisocyanates are desired since the aliphatic diisocyanates generally react too slow. Examples of suitable polyisocyanates include 1,6-diisocyanato hexane, 2,2,4- and/or 2,4,4-trimethyl hexamethylene diisocyanate, p- and m-tetramethyl xylene diisocyanate, dicyclohexylmethane-4,4′-diisocyanate (hydrogenated MDI), 4,4-methylene diphenyl isocyanate (MDI), p- and m-phenylene diisocyanate, 2,4- and/or 2,6-toluene diisocyanate (TDI), durene-1,4-diisocyanate, isophorone diisocyanate, isopropylene-bis-(p-phenyl isocyanate) and sulfone-bis-(p-phenyl isocyanate). Also useful are diisocyanates prepared by capping low molecular weight, that is less than 300, diols, ester diols or diamines with diisocyanates, such as the reaction products of one mole of 1,4-butanediol or bis-(4-hydroxybutyl)-succinate (molecular weight = 262) with two moles of hexamethylene diisocyanate. Any combination of diisocyanates can also be employed. Combinations of slower reacting aliphatic with faster reacting aromatic diisocyanates can be advantageously used. Examples of still other isocyanates include 1,5-naphthalenediisocyanate, cumene-2,4-diisocyanate, 4-methoxy-1,3-phenylenediisocyanate, 4-chloro-1,3-phenylenediisocyanate, 4-bromo-1,3-phenylenediisocyanate, 4-ethoxy-1,3-phenylenediisocyanate, 2,4′-diisocyanatodiphenylether, 4,4′-diphenyldiisocyanate, 4,6-dimethyl-1,3-phenylenediisocyanate, 1,10-anthracenediisocyanate, 4,4′-diisocyanatodibenzyl, 3,3-dimethyl-4,4′-diisocyanatodiphenylmethane, 2,6-dimethyl-4,4′-diisocyanatodiphenyl and mixtures of the same. TDI is desirably utilized. The various diphenylmethane diisocyanates (MDI) and mixtures of MDI with polymeric MDI having an average isocyanate functionality of from about 2 to about 3.2 are preferred.

[0019] Numerous fillers can be utilized in the prepolymer component. The fillers are generally mineral (inorganic), and in a powdery form and serve to adjust the urethane prepolymer adhesive component viscosity as well as to lower the cost thereof. The fillers can at times impart improved adhesion. Examples of specific fillers include ground mica, tale, kaolin clay, calcium carbonate, calcium sulfite, colloidal silica, wollastonite, ballotini, hollow glass microspheres, glass, carbon and graphite fibers, various metallic oxides such as zinc, titanium, zirconium, ground quartz, various metallic silicates, metallic powders such as lead, aluminum, bronze. A preferred filler is talc. The amount of filler is generally an effective amount to produce a viscosity so that the prepolymer component can be readily pumped through processing equipment such as adhesive meter-mixing machines. Such an effective amount is usually from about 5 to about 100 parts by weight and preferably from about 20 to about 50 parts by weight per 100 parts by weight of the prepolymer.

[0020] The curative component contains a polyol having two or more active hydroxyl groups and a primary polyamine. Desirably the curative also contains an inert mineral powdery filler, a polyurethane catalyst, and various pigments or dyes. According to the present invention the amount of curative compound is such that the equivalent ratio of NCO groups of the prepolymer component to OH+NH₂ groups of the curative is from 1.2 to 2.0, desirably 1.35 to 1.6 and preferably 1.35 to 1.45. Such equivalent ranges yield good adhesion to an FRP or to a metal substrate without the need of any surface pretreatment. That is, the surface is treatment-free. By the term "treatment-free" it is meant that the substrate such as the FRP or the metal need not be pre-treated for the adhesion, whether (1) mechanically as by sanding, abrading, (2) with a solvent such as methylene chloride, acetone, toluene, or (3) with a chemical treatment such as through the use of various primers, isocyanates, or amines. The formed adhesive is utilized to bond or adhere FRP to FRP, FRP to a metal, FRP to a painted metal, and FRP to various plastic substrates as for example polyurethane, polyurea, nylon, polydicyclopentadiene, molded epoxy, molded thermoplastic polyesters.

[0021] The curative polyol is a polyol which may be the same as the intermediate polyol utilized to form the prepolymer. Hence, the above description of suitable intermediate polyols is hereby fully incorporated by reference. An essential requirement of the polyol is that it be of a type such that a crosslinked polyurethane adhesive is formed upon cure of the adhesive composition. Thus, if the polyol intermediate and the polyisocyanate used to make the urethane prepolymer are essentially difunctional, the curative polyol should contain sufficient hydroxyls containing more than two OH groups per molecule so that a stable crosslinked network is formed when the curative is utilized. Alternatively, if either the intermediate polyol or the polyisocyanate used to make the prepolymer adhesive base has a functionality significantly greater than 2, the curative polyol may have a functionality of 2, or optionally greater than 2, to form the crosslinked network. Examples of curative polyols include a polyether or a polyester polyol having a molecular weight of from 400 to 10,000, such as the various above-noted polyol intermediates, or triols, tetrols, pentols, hexols, as noted above.

[0022] However, various low molecular weight polyols are generally desired or preferred as the curative component. A class of such polyols include the alkyl, aromatic, or alkyl substituted aromatic diols having from 2 to 12 carbon atoms with from 2 to 8 carbon atoms being preferred. Specific examples include ethylene glycol, propylene glycol, butane diol such as 1,4-butane diol. Another preferred class are the various polyhydric alcohols having from 3 to 15 carbon atoms and preferably from 3 to 10 carbon atoms and from 3 to 8 hydroxyl groups such as triols, tetraols, pentols, hexols, with specific examples including glycerol, erythritol, pentaerythritol, arabitol, sorbitol, trimethylol propane, the various ethylene or propylene oxide adducts of trimethylol propane, glycerol, pentaerythritol, sorbitol. Included within the definition of low molecular weight polyols according to the concepts of the present invention are the various carbohydrates such as the various disaccharides and especially the monosaccharides, along with reaction products thereof with alcohols having from 1 to 5 carbon atoms such as for example alkyl glucoside. Examples of specific disaccharides include sucrose, lactose, and maltose. Examples of monosaccharides include the various pentoses such as arabinose, xylose, lyxose, ribose, as well as the various hexoses such as glucose, gulose, mannose, galactose, talose, allose, altrose, idose, fructose, sorbose can be utilized. Of the various carbohydrates, the various alkyl glucosides with the alkyl group having from 1 to 12 carbon atoms are preferred.

[0023] Examples of preferred polyols include ethylene or propylene oxide adducts of trimethylol propane, pentaerythritol, glycerol, alkyl glucosides, or carbohydrates, with the propylene oxide adduct of pentaerythritol being preferred.

[0024] The inert filler which may be utilized in the curative component can be the same as set forth above. Hence, talc, kaolin clay, and colloidal silica are desired with talc being preferred. The amount of the inorganic inert mineral filler which is utilized in the curative component is an effective amount to produce a viscosity level which can be readily pumped through processing equipment such as adhesive meter mixing machines. Such a level is usually from about 5 parts to about 100 parts by weight and preferably from about 30 to about 60 parts by weight per 100 parts by weight of polyol curative.

[0025] Primary aliphatic polyamines are utilized to provide sag resistance to the adhesive composition or system once the polyol curative component and the urethane prepolymer component are mixed. The primary amine can be a di- or multifunctional primary amine having from 1 to 14 carbon atoms with from 2 to 8 carbon atoms being preferred. Examples of suitable primary amine compounds include diethylenetriamine, ethylenediamine, tetramethylenediamine, pentametylenediamine, hexamethylenediamine, 2,5-diamino-n-hexane, xylene diamine and 1,3-diaminopropanol-2. Generally, ethylene diamine is preferred. The primary amine generally reacts with an equivalent amount of a free isocyanate group (NCO) in the adhesive base to produce a polyurea. The reaction is generally very quick and the polyurea produced forms a strong hydrogen bonded network and significantly increases the viscosity of the mixed adhesive before cure and thereby provides sag resistance. An effective amount of the polyurea is thus utilized to prevent sag in the end product before cure thereof. Such an effective amount is generally from 1 to 5 parts by weight and preferably from 1 to 3 parts by weight per 100 parts by weight of said polyol curative.

[0026] The catalyst used to promote the urethane chain extension and crosslinking reaction is preferably a tin compound such as, for example, various stannous carboxylates like stannous acetate, stannous octoate, stannous laurate, stannous oleate; or dialkyl tin salts of carboxylic acids such as dibutyltin diacetate, dibutyltin dilaurate, dibutyltin maleate, dibutyltin di-2-ethylhexoate, dilauryltin diacetate, dioctyltin diacetate. Similarly, there can be used a trialkyltin hydroxide, dialkyltin oxide or dialkyltin chloride. As an alternative or in addition to the above tin compounds, various tertiary amines can be used such as triethylamine, benzyldimethylamine, triethylenediamine and tetramethylbutanediamine. The tin catalysts, when utilized, are generally used in amounts of 0.5 parts or less, i.e., in the range of about 0.01 to 0.5 part, by weight per 100 parts of prepolymer. The tertiary amine catalysts, when utilized, can be used in amounts of 0.01 to about 5 parts by weight per 100 parts of prepolymer. However, at least 0.01 part of at least one type of catalyst should be present. In addition to the above catalysts, organomercury or organic bismuth compounds can be utilized wherein the organic portion is an aliphatic and preferably an alkyl having from 2 to 20 carbon atoms. The amount is generally from about 0.01 to about 1.0 parts by weight per 100 parts by weight of the prepolymer.

[0027] If it is desired that the polyurethane adhesive composition of the present invention have a color or hue, any conventional pigment or dye can be utilized in conventional amounts. Hence, any pigment known to the art and to the literature can be utilized as for example titanium dioxide, iron oxide, carbon black, as well as various dyes provided that they do not interfere with the urethane reaction.

[0028] The curative component can generally be prepared in any conventional manner. For example, the filler can be added to the curative polyol and mixed therewith. Similarly, the primary amine, the various urethane catalysts, and the various pigments and dyes, if utilized, can also be added and mixed. Generally, any mixing order can be utilized. Similarly, the prepolymer component can be prepared in any conventional manner, for example, the filler can be added to the urethane prepolymer and mixed therewith. The two components can then be added to each other and mixed in a suitable manner as by using meter mixing equipment. The utilization of a primary amine results in an immediate reaction such that a gel is generally formed within 5 minutes and a cure is obtained within from about 20 to about 30 minutes at room temperatures. Generally to ensure the formation of a suitable adhesive bond within a relatively short time, that is generally les than 5 minutes and preferably less than 1 minute, the mixed urethane prepolymer component and curative component are heated to a temperature of at least 50°C and preferably from about 90° to about 125°C. Naturally, the reaction time to form a suitable bond will depend upon the particular type of polyisocyanate utilized, the particular type of polyol curative utilized, the particular type of urethane catalyst utilized, the curing temperature, and the like.

[0029] The urethane adhesive compositions of the present invention are suitable for application to non-treated or surface-treatment free substrates such as FRP substrates, metal substrates, plastic substrates. The adhesive of the present invention can thus be utilized to bond at least two such substrates together to form a urethane adhesive composite. An area of particular use is in the automotive industry wherein FRP structural components are bonded to automobile body panels such as hoods, doors, fenders, front ends, trunk lids.

[0030] The invention will be better understood by reference to the following examples.

EXAMPLES

[0031] Examples 1 and 2 describe the preferred method of making the two adhesive components (base and curative). Example 3 describes the preparation of adhesive test specimens while Example 4 describes the specimen test procedures. The test results for specimens made at various isocyanate indices (both primed and unprimed) are shown in Example 5 (Table 1). It is clear from the data that adhesives mixed at an isocyanate index of 1.38 and 1.50 gave superior adhesion even when the FRP surfaces are unprimed. Example 6 (Table 2) shows that the adhesive mixed at an isocyanate index of 1.40 gave bonds to FRP (both primed and unprimed) which are resistant to the water immersion test. Example 7 (Table 3) shows that adhesively bonded FRP also has excellent adhesion at minus 40°C. An additional concern is that moisture can be absorbed on the FRP surface (particularly in a plant production environment) and that this absorbed moisture can adversely affect adhesive bonding, in particular when there is no precleaning of the FRP surface. In Example 8, FRP specimens were placed in a high humidity environment for 24 hours prior to bonding. The data in Table 4 shows that a high equivalent ratio of free isocyanate to amine and hydroxyl groups yields improved adhesion to non-treated humidified FRP samples, better than to treated surfaces using an adhesive having an equivalent ratio of 1.10. Hence, rather than yielding reduction in adhesion to a non-treated surface as would be expected, the result of improved adhesion was unexpected. The performance of the high isocyanate index adhesive, that is the equivalent ratio of free prepolymer component NCO groups to hydroxyl and NH₂ groups of the curative component, was compared with adhesive mixed at a normal index at a high temperature. Since curing of the high index adhesive could result in some allophanate crosslinking, there may be a concern about performance at elevated temperatures such as that encountered in paint ovens. The data in Table 5, however, shows that the high index adhesive performed very well at a high temperature (166°C). Peel adhesion has been previously shown to be a problem if a two-component polyurethane adhesive is applied to unprimed FRP. The data in Example 10 (Table 6) shows that the adhesive mixed at a high index (1.40) has excellent peel adhesion in the Wedge Peel Test.

[0032] All parts set forth in the examples are by weight unless otherwise indicated.

Example 1

[0033] A polyurethane prepolymer was prepared using the following procedure: polypropylene ether diol, 3000 molecular weight (41.4 parts), and styrenated diphenylamine (0.40 parts), were charged to a clean, dry reactor. The reactor and its contents were heated with stirring to 110°C. During the heating cycle, powdered talcum (28.2 parts), was added. The reactor was heated to 110°C under vacuum (5 mm) for 2 hours. The contents of the reactor were sampled and analyzed by Karl Fischer titration for water (≦0.09% H₂O). The reactor was evacuated and 15.0 parts of methylene bis(4-phenyl isocyanate) (MDI) containing higher molecular weight oligomers of MDI was added. The contents of the reactor were mixed for 2 hours at 110°C when an additional 15.0 parts of the above isocyanate mixture was added. The contents of the reactor were mixed and then cooled to 30°C under vacuum. The NCO content of the final product is 1.92 meq/gm and the viscosity was 16,400 cps (Brookfield). The adhesive base was used in all subsequent experiments.

Example 2

[0034] Several polyurethane curatives were prepared using the following procedure: A polyol, propylene oxide adduct of pentaerythritol (63.55 parts), and phthalocyanine blue (0.75 parts), were charged to a clean, dry reactor. The reactor was heated to 110°C while adding powdered talcum (34.25 parts). The polyol/talc slurry was heated at 110°C under vacuum for 2 hours. A sample was removed for water analysis by Karl Fischer titration (<0.15% H₂O). The reactor was cooled to 65°C and ethylenediamine, (1.20 parts), and dibutyltin dilaurate catalyst, (0.25 gms), were added. The mixture was stirred and cooled to 30°C. The final product had a viscosity of 8,000 cps (Brookfield). This curative was used with the adhesive base described in Example 1 at a base/curative mix ratio of 3.2/1 to form the final polyurethane adhesive. Several other curatives were prepared in the same way for use at other mix ratios except that the levels of dibutyltin dilaurate catalyst and ethylenediamine were adjusted to give the same level of these ingredients in the final mixed adhesive.

Example 3

[0035] For testing of adhesive strength, standard lap shear specimens were prepared using the following procedure: FRP panels of 356 x 356 x 2.5mm (14" x 14" x 0.1") were press molded from a sheet molding compound (glass fiber reinforced unsaturated polyester/styrene). These panels were cut into 102 x 152mm (4" x 6") plaques using a diamond tipped circular saw. Polyurethane adhesive was mixed from the components described in Examples 1 and 2 using adhesive meter-mixing equipment (Model MVR-28 available from Liquid Control Corp.) equipped with a static type mixing head. A bead of mixed adhesives 152mm (6") long was applied along one side of a 102 x 152mm (4" x 6") FRP plaque. The plaque was placed in an aluminum fixture and a second plaque was aligned on top of the adhesive bead to give a final specimen 152 x 152mm (6" x 6") with a 25 x 152mm (1" x 6") overlap bonded area. The aluminum fixture was designed to give a standard 0.89mm (.035")bond line thickness. The fixture with the bonded sample was placed in an air circulating oven at 125°C for 30 minutes to cure the adhesive. The bonded specimen was removed from the fixture and excess adhesive was removed from the specimen edges using a knife. The final specimen was placed in an air circulating oven at 150°C for 1 hour to ensure complete cure. The resultant 152 x 152mm (6" x 6") specimens were then cut into the final test samples (25 x 152mm with a 25mm bonded overlap area) using a diamond tipped circular saw. Before bonding, some of the samples were primed with a 2% solution of polymeric diphenylmethane diisocyanate. The primer was applied to the surface of the FRP using a chemically resistant paint brush.

Example 4

[0036] The lap shear adhesive samples were tested using standard Instron type testing equipment with a crosshead speed of 21µms⁻¹ (0.05"/minute). The Instron had the capability to test at both high and low temperatures. In some cases, samples were tested at 80°C, 166°C and minus 40°C as well as at room temperature. The resistance of the adhesive bonds to water was determined by conditioning the samples before testing using a water immersion procedure (7 days in water at 54°C). Samples were tested immediately after removal from the water as well as after an additional 24-hour period in which the samples were exposed to ambient conditions. In addition, in some cases samples were made and tested using FRP which was conditioned at 92% relative humidity before application of adhesion.

Example 5

[0037] Lap shear adhesive test specimens were prepared using adhesives (Examples 1 and 2) mixed at different mix ratios. This resulted in mixed adhesives of varying isocyanate index. The results for both primed and unprimed samples tested at 82°C are listed in Table I for adhesives of varying isocyanate index.

Example 6

[0038] Lap shear adhesive test specimens (both primed and unprimed) were prepared using adhesive mixed at an isocyanate index of 1.40. The specimens were subjected to the water immersion procedure (Example 4) before testing. Results are shown in Table II and compared with samples which were not subjected to water immersion.

Example 7

[0039] Lap shear adhesion test specimens, both primed and unprimed, were prepared using adhesive mixed at an isocyanate index of 1.40. The specimens were tested at minus 40°C to determine the adhesion at low temperatures. The results are shown in Table III.

Example 8

[0040] FRP plaques to be used for bonding were placed in a constant humidity chamber (92% relative humidity at 20°C). After 24 hours, the plaques were taken from the constant humidity chamber and immediately fabricated into lap shear adhesive test specimens. The samples were tested under different conditions and the results were compared with those from FRP which had not been humidified. The results for the various tests are shown in Table IV.

Example 9

[0041] Lap shear adhesion samples were fabricated using adhesives mixed at isocyanate indices of 1.40 and 1.12 using the procedures described in Examples 1-3. Lap shear adhesion was determined at 166°C for both primed and unprimed samples. Results are given in Table V.

Example 10

[0042] Samples were prepared for evaluation using a Wedge Peel Test. In this test, two 152 x 152mm (6" x 6") plaques of FRP are bonded together at one edge 51 x 152 x 0.89mm (2" x 6" x .035") adhesively bonded area. A steel wedge 152mm (6") long with a 45° angle is attached to an Instron. The wedge is brought into contact with the open end of the bonded specimen. The specimen is mounted in a support on the Instron and carefully aligned in a vertical position. The Instron speed is set at 4.2mms⁻¹ (10"/minute). After testing, the mode of failure is noted as well as the force required for failure. Results for the Wedge Peel Test are given in Table VI.

TABLE I

LAP SHEAR ADHESION FOR VARYING ISOCYANATE INDEX
Sample No.	Priming	NCO/OH+NH₂	Adhesive* Strength (MNm⁻²/PSI)	Sample Failure Mode
1A	+	1.12	1.99 ± 0.10/288 ± 15	AF
1B	-	1.12	1.48 ± 0.19/214 ± 27	AF
1C	+	1.25	2.69 ± 0.05/390 ± 7.5	SFD
1D	-	1.25	1.89 ± 0.12/274 ± 17	AF
1E	+	1.38	2.85 ± 0.12/414 ± 17	SFD
1F	-	1.38	2.86 ± 0.18/415 ± 26	SFD
1G	+	1.50	2.39 ± 0.23/347 ± 33	SFD
1H	-	1.50	2.65 ± 0.26/385 ± 38	SFD

* Average of 5 samples each condition

AF = Adhesive Failure SFD = Failure by delamination of the FRP substrate.

TABLE III

LAP SHEAR ADHESION AT -40°C
Sample No.	Priming	NCO/OH+NH₂	Adhesive* Strength (MNm⁻²/PSI)	Sample Failure Mode
3A	-	1.40	3.39 ± 0.26/492 ± 38	SFD
3B	+	1.40	3.77 ± 0.19/547 ± 27	SFD

* Average of 5 samples

[0043] 

TABLE V

LAP SHEAR ADHESION : HIGH TEMPERATURE
Sample No.	Priming	NCO/OH+NH₂	Test Temp. (°C)	Adhesive* Strength (MNm⁻²/PSI)	Sample Failure Mode
5A	+	1.40	166	0.62 ± 0.15/90 ± 22	AF
5B	-	1.40	166	0.52 ± 0.05/76 ± 7	AF
5C	+	1.12	166	0.46 ± 0.05/66 ± 7	AF
5D	-	1.12	166	0.33 ± 0.03/48 ± 5	AF

* Average of 5 samples

[0044] 

TABLE VI

WEDGE PEEL TEST
Sample No.	Priming	NCO/OH+NH₂	Maximum Force (N/lbf)	Sample Failure Mode
6A	-	1.40	430/96	SFD
6B	-	1.40	170/39	SFD
6C	+	1.40	230/51	SFD
6D	+	1.40	220/49	SFD

Claims

Claims for the following Contracting State(s): BE, DE, FR, GB, IT, LU, NL

1. A two-component urethane adhesive, having

(a) a urethane prepolymer component, made from polyol intermediate and polyisocyanate with the polyisocyanate at equivalent ratio of at least 2 to give free NCO groups in the prepolymer component, and

(b) a curative component comprising curative polyol and primary polyamine,

   the urethane prepolymer component and the curative component being reactive together to form a crosslinked polyurethane;
characterised in that
   the relative amounts of components (a) and (b) are such that the equivalent ratio [NCO:(OH+NH₂)] of free prepolymer NCO groups in the prepolymer component to the polyol OH and primary polyamine NH₂ in the curative component is from 1.2 to 2.0.

2. An adhesive according to claim 1 in which the equivalent ratio [NCO:(OH+NH₂)] is at least 1.25.

3. An adhesive according to claim 2 in which the equivalent ratio [NCO:(OH+NH₂)] is in the range 1.35 to 1.6.

4. An adhesive according to any one of the preceding claims in which the polyol of the curative component (b) comprises nitrogen-free polyether polyol or nitrogen-free polyester polyol.

5. An adhesive according to claim 4 in which the polyether polyol or polyester polyol has a number average molecular weight of from 400 to 10000.

6. An adhesive according to any one of the preceding claims in which the curative polyol comprises a nitrogen-free low molecular weight polyol selected from C₂₋₁₂ diols, C₃₋₁₅ polyhydric alcohols having 3 to 8 OH groups, carbohydrates, and combinations of any of these.

7. An adhesive according to claim 6 in which the nitrogen-free low molecular weight polyol is an ethylene oxide adduct or propylene oxide adduct of trimethylol propane or pentaerythritol, or an alkyl glucoside.

8. An adhesive according to any one of the preceding claims in which, in the prepolymer component (a), said equivalent ratio of isocyanate to polyol intermediate is in the range 5 to 10.

9. An adhesive according to any one of the preceding claims in which the prepolymer component (a) is made from polyisocyanate comprising polyisocyanate of the formula R(NCO)_n where n = 2, 3 or 4 and R is C₆₋₂₀ aromatic.

10. An adhesive according to any one of the preceding claims in which the prepolymer component (a) is made from polyol intermediate which is polyester polyol or polyether polyol, having a number average molecular weight in the range 400 to 10000, preferably 2000 to 4000.

11. An adhesive according to claim 10 in which said polyester polyol is made from C₂₋₁₅ polyhydric alcohol and C₂₋₁₄ polycarboxylic acid.

12. An adhesive according to claim 10 in which the polyol intermediate is polypropylene ether diol, poly-1,2-butylene ether diol, poly-1,4-tetramethylene ether diol, ε-polycaprolactone diol, or a mixture of these.

13. An adhesive according to any one of the preceding claims in which the prepolymer component and/or the curative component includes filler.

14. An adhesive according to any one of the preceding claims in which the primary polyamine in the curative component is a C₁₋₁₄ aliphatic amine.

15. An adhesive according to claim 14 in which said primary polyamine is ethylene diamine.

16. An adhesive according to any one of the preceding claims in which 1 to 5 parts by weight of the primary polyamine is present per 100 parts curative polyol in the curative component.

17. An adhesive according to any one of the preceding claims in which the curative component (b) includes catalyst for urethane-forming reaction.

18. A process comprising adhering two articles together using a two-component urethane adhesive according to any one of claims 1 to 17.

19. A process according to claim 18 in which one or both of the adhered surfaces of the articles is treatment-free for the adhesion.

20. A process according to claim 18 or claim 19 in which one or both articles is of fibre-reinforced plastics.

21. A process according to any one of claims 18 to 20 in which the adhesive is cured by heating to above 50°C.

22. An adhered composite obtained by a process according to any one of claims 18 to 21.

Claims

Claims for the following Contracting State(s): ES

1. A method of making a two-component urethane adhesive, comprising mixing

(a) a urethane prepolymer component, made from polyol intermediate and polyisocyanate with the polyisocyanate at equivalent ratio of at least 2 to give free NCO groups in the prepolymer component, and

(b) a curative component comprising curative polyol and primary polyamine,

   the urethane prepolymer component and the curative component being reactive together to form a crosslinked polyurethane;
characterised in that
   the relative amounts of components (a) and (b) are such that the equivalent ratio [NCO:(OH+NH₂)] of free prepolymer NCO groups in the prepolymer component to the polyol OH and primary polyamine NH₂ in the curative component is from 1.2 to 2.0.

2. A method according to claim 1 in which the equivalent ratio [NCO:(OH+NH₂)] is at least 1.25.

3. A method according to claim 2 in which the equivalent ratio [NCO:(OH+NH₂)] is in the range 1.35 to 1.6.

4. A method according to any one of the preceding claims in which the polyol of the curative component (b) comprises nitrogen-free polyether polyol or nitrogen-free polyester polyol.

5. A method according to claim 4 in which the polyether polyol or polyester polyol has a number average molecular weight of from 400 to 10000.

6. A method according to any one of the preceding claims in which the curative polyol comprises a nitrogen-free low molecular weight polyol selected from C₂₋₁₂ diols, C₃₋₁₅ polyhydric alcohols having 3 to 8 OH groups, carbohydrates, and combinations of any of these.

7. A method according to claim 6 in which the nitrogen-free low molecular weight polyol is an ethylene oxide adduct or propylene oxide adduct of trimethylol propane or pentaerythritol, or an alkyl glucoside.

8. A method according to any one of the preceding claims in which, in the prepolymer component (a), said equivalent ratio of isocyanate to polyol intermediate is in the range 5 to 10.

9. A method according to any one of the preceding claims in which the prepolymer component (a) is made from polyisocyanate comprising polyisocyanate of the formula R(NCO)_n where n = 2, 3 or 4 and R is C₆₋₂₀ aromatic.

10. A method according to any one of the preceding claims in which the prepolymer component (a) is made from polyol intermediate which is polyester polyol or polyether polyol, having a number average molecular weight in the range 400 to 10000, preferably 2000 to 4000.

11. A method according to claim 10 in which said polyester polyol is made from C₂₋₁₅ polyhydric alcohol and C₂₋₁₄ polycarboxylic acid.

12. A method according to claim 10 in which the polyol intermediate is polypropylene ether diol, poly-1,2-butylene ether diol, poly-1,4-tetramethylene ether diol, ε-polycaprolactone diol, or a mixture of these.

13. A method according to any one of the preceding claims in which the prepolymer component and/or the curative component includes filler.

14. A method according to any one of the preceding claims in which the primary polyamine in the curative component is a C₁₋₁₄ aliphatic amine.

15. A method according to claim 14 in which said primary polyamine is ethylene diamine.

16. A method according to any one of the preceding claims in which 1 to 5 parts by weight of the primary polyamine is present per 100 parts curative polyol in the curative component.

17. A method according to any one of the preceding claims in which the curative component (b) includes catalyst for urethane-forming reaction.

18. A process comprising adhering two articles together using a two-component urethane adhesive according to any one of claims 1 to 17.

19. A process according to claim 18 in which one or both of the adhered surfaces of the articles is treatment-free for the adhesion.

20. A process according to claim 18 or claim 19 in which one or both articles is of fibre-reinforced plastics.

21. A process according to any one of claims 18 to 20 in which the adhesive is cured by heating to above 50°C.

22. An adhered composite obtained by a process according to any one of claims 18 to 21.

Ansprüche

Patentansprüche für folgende(n) Vertragsstaat(en): BE, DE, FR, GB, IT, LU, NL

1. Zweikomponenten-Urethanklebstoff umfassend

(a) eine Urethanpräpolymer-Komponente, die aus einem Polyolzwischenprodukt und Polyisocyanat hergestellt ist, wobei das Polyisocyanat in einem Äquivalenzverhältnis von zumindest 2 vorliegt, um freie NCO-Gruppen in der Präpolymerkomponente zu ergeben und

(b) eine Härterkomponente umfassend Härterpolyol und primäres Polyamin,

wobei die Urethanpräpolymer-Komponente und die Härterkomponente miteinander reaktiv sind, um ein vernetztes Polyurethan zu bilden;
dadurch gekennzeichnet, daß
die relativen Mengen der Komponenten (a) und (b) solcherart sind, daß das Äquivalenzverhältnis [NCO:(OH+NH₂)] freier Präpolymer-NCO-Gruppen in der Präpolymerkomponente zu OH im Polyol und NH₂ im primären Polyamin in der Härterkomponente zwischen 1,2 und 2,0 liegt.

2. Klebstoff nach Anspruch 1, worin das Äquivalenzverhältnis [NCO:(OH+NH₂)] zumindest 1,25 beträgt.

3. Klebstoff nach Anspruch 2, worin das Äquivalenzverhältnis [NCO:(OH+NH₂)] im Bereich von 1,35 bis 1,6 liegt.

4. Klebstoff nach einem der vorhergehenden Ansprüche, worin das Polyol der Härterkomponente (b) stickstofffreies Polyätherpolyol oder stickstofffreies Polyesterpolyol umfaßt.

5. Klebstoff nach Anspruch 4, worin das Polyätherpolyol oder Polyesterpolyol ein Zahlendurchschnitts-Molekulargewicht von 400 bis 10.000 hat.

6. Klebstoff nach einem der vorhergehenden Ansprüche, worin das Härterpolyol ein stickstofffreies Polyol mit niedrigem Molekulargewicht umfaßt, ausgewählt aus C₂₋₁₂ Diolen, C₃₋₁₅ mehrwertigen Alkoholen mit 3 bis 8 OH-Gruppen, Kohlehydraten und Kombinationen von beliebigen von diesen.

7. Klebstoff nach Anspruch 6, worin das stickstofffreie Polyol mit niedrigem Molekulargewicht ein Äthylenoxid-Addukt oder Propylenoxid-Addukt von Trimethylolpropan oder Pentaerythrit, oder ein Alkylglucosid ist.

8. Klebstoff nach einem der vorhergehenden Ansprüche, worin in der Präpolymerkomponente (a) das genannte Äquivalenzverhältnis von Isocyanat zu Polyol-Zwischenprodukt im Bereich von 5 bis 10 liegt.

9. Klebstoff nach einem der vorhergehenden Ansprüche, worin die Präpolymerkomponente (a) aus Polyisocyanat besteht, umfassend Polyisocyanat der Formel R(NCO)_n, worin n = 2, 3 oder 4 und R ein C₆₋₂₀ Aromat ist.

10. Klebstoff nach einem der vorhergehenden Ansprüche, worin die Präpolymerkomponente (a) aus einem Polyol-Zwischenprodukt hergestellt ist, das Polyesterpolyol oder Polyätherpolyol mit einem Zahlendurchschnitts-Molekulargewicht im Bereich von 400 bis 10.000, vorzugsweise 2.000 bis 4.000 ist.

11. Klebstoff nach Anspruch 10, worin das Polyesterpolyol aus C₂₋₁₅ mehrwertigem Alkohol und C₂₋₁₄ Polycarbonsäure hergestellt ist.

12. Klebstoff nach Anspruch 10, worin das Polyol-Zwischenprodukt Polypropylen-Ätherdiol, Poly-1,2-Butylenätherdiol, Poly-1,4-Tetramethylen-ätherdiol, ε-Polycaprolactondiol oder eine Mischung von diesen ist.

13. Klebstoff nach einem der vorhergehenden Ansprüche, worin die Präpolymerkomponente und/oder die Härterkomponente einen Füllstoff enthält.

14. Klebstoff nach einem der vorhergehenden Ansprüche, worin das primäre Polyamin in der Härterkomponente ein C₁₋₁₄ aliphatisches Amin ist.

15. Klebstoff nach Anspruch 14, worin das primäre Polyamin Äthylendiamin ist.

16. Klebstoff nach einem der vorhergehenden Ansprüche, worin 1 bis 5 Gew.-Teile des primären Polyamins pro 100 Teile Härterpolyol in der Härterkomponente vorhanden sind.

17. Klebstoff nach einem der vorhergehenden Ansprüche, worin die Härterkomponente (b) einen Katalysator zur Urethanbildungsreaktion enthält.

18. Verfahren umfassend das Zusammenkleben von zwei Gegenständen unter Verwendung eines Zweikomponenten-Urethanklebstoffs nach einem der Ansprüche 1 bis 17.

19. Verfahren nach Anspruch 18, worin eine oder beide der zusammengeklebten Oberflächen der Gegenstände für das Kleben behandlungsfrei ist/sind.

20. Verfahren nach Anspruch 18 oder Anspruch 19, worin einer oder beide Gegenstände aus faserverstärkten Kunststoffen besteht/bestehen.

21. Verfahren nach einem der Ansprüche 18 bis 20, worin der Klebstoff durch Erwärmung auf über 50°C gehärtet wird.

22. Geklebter Verbundstoff, der durch ein Verfahren nach einem der Ansprüche 18 bis 21 gewonnen wird.

Ansprüche

Patentansprüche für folgende(n) Vertragsstaat(en): ES

1. Verfahren zum Herstellen eines Zweikomponenten-Urethanklebstoffes, umfassend das Mischen

(a) einer Urethanpräpolymer-Komponente hergestellt aus einem Polyol-Zwischenprodukt und Polyisocyanat, wobei das Polyisocyanat in einem Äquivalenzverhältnis von zumindest 2 vorliegt, um freie NCO-Gruppen in der Präpolymerkomponente zu ergeben,
und

(b) einer Härterkomponente umfassend Härterpolyol und primäres Polyamin,

wobei die Urethanpräpolymer-Komponente und die Härterkomponente miteinander reaktiv sind, um ein vernetztes Polyurethan zu bilden;
dadurch gekennzeichnet, daß
die relativen Mengen der Komponenten (a) und (b) solcherart sind, daß das Äquivalenzverhältnis [NCO: (OH+NH₂)] freier Präpolymer-NCO-Gruppen in der Präpolymerkomponente zu OH in Polyol und NH₂ im primären Polyamin in der Härterkomponente zwischen 1,2 und 2,0 liegt.

2. Verfahren nach Anspruch 1, worin das Äquivalenzverhältnis [NCO: (OH+NH₂)] zumindest 1,25 ist.

3. Verfahren nach Anspruch 2, worin das Äquivalenzverhältnis [NCO: (OH+NH₂)] im Bereich von 1,35 bis 1,6 liegt.

4. Verfahren nach einem der vorhergehenden Ansprüche, worin das Polyol in der Härterkomponente (b) stickstofffreies Polyätherpolyol oder stickstofffreies Polyesterpolyol umfaßt.

5. Verfahren nach Anspruch 4, worin das Polyätherpolyol oder Polyesterpolyol ein Zahlendurchschnitts-Molekulargewicht von 400 bis 10.000 hat.

6. Verfahren nach einem der vorhergehenden Ansprüche, worin das Härterpolyol ein stickstofffreies Polyol mit niedrigem Molekulargewicht umfaßt, ausgewählt aus C₂₋₁₂ Diolen, C₃₋₁₅ mehrwertigen Alkoholen mit 3 bis 8 OH-Gruppen, Kohlehydraten und Kombinationen von beliebigen von diesen.

7. Verfahren nach Anspruch 6, worin das stickstofffreie Polyol mit niedrigem Molekulargewicht ein Äthylenoxid-Addukt oder Propylenoxid-Addukt von Trimethylolpropan oder Pentaerythrit, oder ein Alkylglucosid ist.

8. Verfahren nach einem der vorhergehenden Ansprüche, worin in der Präpolymerkomponente (a) das Äquivalenzverhältnis von Isocyanat zum Polyol-Zwischenprodukt im Bereich von 5 bis 10 liegt.

9. Verfahren nach einem der vorhergehenden Ansprüche, worin die Präpolymerkomponente (a) aus Polyisocyanat besteht, umfassend Polyisocyanat der Formel R(NCO)_n, worin n = 2, 3 oder 4 und R ein C₆₋₂₀ Aromat ist.

10. Verfahren nach einem der vorhergehenden Ansprüche, worin die Präpolymerkomponente (a) aus einem Polyol-Zwischenprodukt hergestellt ist, das Polyesterpolyol oder Polyätherpolyol mit einem Zahlendurchschnitts-Molekulargewicht im Bereich von 400 bis 10.000, vorzugsweise 2.000 bis 4.000 ist.

11. Verfahren nach Anspruch 10, worin das Polyesterpolyol aus C₂₋₁₅ mehrwertigem Alkohol und C₂₋₁₄ Polycarbonsäure hergestellt ist.

12. Verfahren nach Anspruch 10, worin das Polyol-Zwischenprodukt Polypropylen-ätherdiol, Poly-1,2-Butylenätherdiol, Poly-1,4-Tetramethylen-ätherdiol, ε-Polycaprolactondiol oder eine Mischung von diesen ist.

13. Verfahren nach einem der vorhergehenden Ansprüche, worin die Präpolymerkomponente und/oder die Härterkomponente einen Füllstoff enthält.

14. Verfahren nach einem der vorhergehenden Ansprüche, worin das primäre Polyamin in der Härterkomponente ein C₁₋₁₄ aliphatisches Amin ist.

15. Verfahren nach Anspruch 14, worin das primäre Polyamin Äthylendiamin ist.

16. Verfahren nach einem der vorhergehenden Ansprüche, worin 1 bis 5 Gew.-Teile des primären Polyamins pro 100 Teile Härterpolyol in der Härterkomponente vorhanden sind.

17. Verfahren nach einem der vorhergehenden Ansprüche, worin die Härterkomponente (b) einen Katalysator zur Urethanbildungsreaktion enthält.

18. Verfahren umfassend das Zusammenkleben von zwei Gegenständen unter Verwendung eines Zweikomponenten-Urethanklebstoffs nach einem der Ansprüche 1 bis 17.

19. Verfahren nach Anspruch 18, worin eine oder beide der zusammengeklebten Oberflächen der Gegenstände für das Kleben behandlungsfrei ist/sind.

20. Verfahren nach Anspruch 18 oder Anspruch 19, worin ein oder beide Gegenstände aus faserverstärkten Kunststoffen besteht/bestehen.

21. Verfahren nach einem der Ansprüche 18 bis 20, worin der Klebstoff durch Erwärmen auf über 50°C gehärtet wird.

22. Geklebter Verbundstoff, der durch ein Verfahren nach einem der Ansprüche 18 bis 21 gewonnen wird.

Revendications

Revendications pour l'(les) Etat(s) contractant(s) suivant(s): BE, DE, FR, GB, IT, LU, NL

1. Adhésif de polyuréthane à deux composants, ayant

(a) un composant prépolymère uréthane, fabriqué à partir d'un intermédiaire polyol et d'un polyisocyanate avec le polyisocyanate à un rapport équivalent d'au moins 2 pour donner des groupes NCO libres dans le composant prépolymère, et

(b) un composant de polymérisation comprenant un polyol polymérisant et une polyamine primaire,

   le composant prépolymère uréthane et le composant polymérisant étant réactif ensemble pour former un polyuréthane réticulé;
   caractérisé en ce que
   les quantités relatives des composants (a) et (b) sont telles que le rapport équivalent [NCO : (OH+NH₂)] des groupes NCO libres du prépolymère dans le composant prépolymère aux OH du polyol et aux NH₂ de la polyamine primaire dans le composant de polymérisation est de 1,2 à 2,0.

2. Adhésif selon la revendication 1, dans lequel le rapport équivalent [NCO : (OH+NH₂)] est d'au moins 1,25.

3. Adhésif selon la revendication 2, dans lequel le rapport équivalent [NCO : (OH+NH₂)] est dans l'intervalle de 1,35 à 1,6.

4. Adhésif selon l'une quelconque des revendications précédentes dans lequel le polyol du composant de polymérisation (b) comprend un polyol de polyéther exempt d'azote ou un polyol de polyester exempt d'azote.

5. Adhésif selon la revendication 4, dans lequel le polyol de polyéther ou le polyol de polyester a un nombre de poids moléculaire moyen de 400 à 10000.

6. Adhésif selon l'une quelconque des revendications précédentes, dans lequel le polyol de polymérisation comprend un polyol de bas poids moléculaire exempt d'azote choisi parmi les diols en C₂₋₁₂, les alcools polyhydriques en C₃₋₁₅ ayant de 3 à 8 groupes OH, les carbohydrates, et les combinaisons de ceux-ci.

7. Adhésif selon la revendication 6, dans lequel le polyol de bas poids moléculaire exempt d'azote est un composé d'addition oxyde d'éthylène ou un composé d'addition oxyde de propylène de triméthylol propane ou de pentaérythritol, ou un alkyl glucoside.

8. Adhésif selon l'une quelconque des revendications précédentes dans lequel, dans le composant prépolymère (a), ledit rapport équivalent d'isocyanate à l'intermédiaire polyol est dans l'intervalle de 5 à 10.

9. Adhésif selon l'une quelconque des revendications précédentes dans lequel le composant prépolymère (a) est fabriqué à partir de polyisocyanate comprenant un polyisocyanate de la formule R(NCO)_n où n = 2, 3 ou 4 et R est un aromatique en C₆₋₂₀.

10. Adhésif selon l'une quelconque des revendications précédentes dans lequel le composant prépolymère (a) est fabriqué à partir d'un intermédiaire polyol qui est un polyester polyol ou un polyéther polyol, ayant un nombre de poids moléculaire moyen dans l'intervalle de 400 à 10000, de préférence de 2000 à 4000.

11. Adhésif selon la revendication 10, dans lequel ledit polyester polyol est fabriqué à partir d'un alcool polyhydrique en C₂₋₁₅ et d'un acide polycarboxylique en C₂₋₁₄.

12. Adhésif selon la revendication 10, dans lequel l'intermédiaire polyol est le polypropylène éther diol, le poly-1,2-butylène éther diol, le poly-1,4-tétraméthylène éther diol, le ε-polycaprolactone diol, ou un mélange de ceux-ci.

13. Adhésif selon l'une quelconque des revendications précédentes dans lequel le composant prépolymère et/ou le composant de polymérisation inclut une charge.

14. Adhésif selon l'une quelconque des revendications précédentes, dans lequel la polyamine primaire dans le composant de polymérisation est une amine aliphatique en C₁-₁₄.

15. Adhésif selon la revendication 14, dans lequel ladite polyamine primaire est une éthylène diamine.

16. Adhésif selon l'une quelconque des revendications précédentes dans lequel 1 à 5 parties en poids de la polyamine primaire sont présentes pour 100 parties de polyol de polymérisation dans le composant de polymérisation.

17. Adhésif selon l'une quelconque des revendications précédentes dans lequel le composant de polymérisation (b) inclut un catalyseur pour la réaction de formation de l'uréthane.

18. Procédé comprenant le collage de deux articles ensemble en utilisant un adhésif à base d'uréthane à deux composants selon l'une quelconque des revendications 1 à 17.

19. Procédé selon la revendication 18, dans lequel une ou les deux surfaces collées des articles est exempte de traitement pour l'adhésion.

20. Procédé selon la revendication 18 ou la revendication 19, dans lequel un ou les deux articles sont des plastiques renforcés par des fibres.

21. Procédé selon l'une quelconque des revendications 18 à 20, dans lequel l'adhésif est polymérisé par chauffage au-dessus de 50°C.

22. Composite collé obtenu par un procédé selon l'une quelconque des revendications 18 à 21.

Revendications

Revendications pour l'(les) Etat(s) contractant(s) suivant(s): ES

1. Méthode de fabrication d'un adhésif d'uréthane à deux composants, comprenant le mélange de

(a) un composant prépolymère uréthane, fabriqué à partir d'un intermédiaire polyol et d'un polyisocyanate avec le polyisocyanate à un rapport équivalent d'au moins 2 pour donner des groupes NCO libres dans le composant prépolymère, et

(b) un composant de polymérisation comprenant un polyol de polymérisation et une polyamine primaire,

   le composant prépolymère uréthane et le composant de polymérisation étant réactif ensemble pour former un polyuréthane réticulé;
   caractérisé en ce que
   les quantités relatives des composants (a) et (b) sont telles que le rapport équivalent [NCO : (OH+NH₂)] des groupes NCO libres du prépolymère dans le composant prépolymère aux OH du polyol et aux NH₂ de la polyamine primaire dans le composant de polymérisation et de 1,2 à 2,0.

2. Méthode selon la revendication 1, dans laquelle le rapport équivalent [NCO : (OH+NH₂)] est d'au moins 1,25.

3. Méthode selon la revendication 2, dans laquelle le rapport équivalent [NCO : (OH+NH₂)] est dans l'intervalle de 1,35 à 1,6.

4. Méthode selon l'une quelconque des revendications précédentes, dans laquelle le polyol du composant de polymérisation (b) comprend un polyéther polyol exempt d'azote ou un polyester polyol exempt d'azote.

5. Méthode selon la revendication 4, dans laquelle le polyéther polyol ou le polyester polyol a un nombre de poids moléculaire moyen de 400 à 10000.

6. Méthode selon l'une quelconque des revendications précédentes dans laquelle le polyol de polymérisation comprend un polyol à bas poids moléculaire exempt d'azote choisi parmi les diols en C₂₋₁₂, les alcools polyhydriques en C₃₋₁₅ ayant 3 à 8 groupes OH, les carbohydrates, et les combinaisons de ceux-ci.

7. Méthode selon la revendication 6, dans laquelle le polyol a bas poids moléculaire exempt d'azote est un produit d'addition oxyde d'éthylène ou un produit d'addition d'oxyde de propylène d'un triméthylol propane ou d'un pentaerythritol, ou un alkyl glucoside.

8. Méthode selon l'une quelconque des revendications précédentes dans laquelle, dans le composant prépolymère (a), ledit rapport équivalent d'isocyanate à l'intermédiaire polyol est dans l'intervalle de 5 à 10.

9. Méthode selon l'une quelconque des revendications précédentes dans laquelle le composant prépolymère (a) est fabriqué à partir de polyisocyanate comprenant un polyisocyanate de la formule R(NCO)_n où n = 2, 3 ou 4 et R est un aromatique en C₆₋₂₀.

10. Méthode selon l'une quelconque des revendications précédentes dans lequel le composant prépolymère (a) est fabriqué à partir d'un intermédiaire polyol qui est un polyester polyol ou un polyéther polyol, ayant un nombre de poids moléculaire moyen dans l'intervalle de 400 à 10000, de préférence 2000 à 4000.

11. Méthode selon la revendication 10, dans laquelle ledit polyester polyol est fabriqué à partir d'un alcool polyhydrique en C₂₋₁₅ et d'un acide polycarboxylique en C₂₋₁₄.

12. Méthode selon la revendication 10, dans laquelle l'intermédiaire polyol est le polypropylène éther diol, le poly-1,2-butylène éther diol, le poly-1,4-tetraméthylène éther diol, le ε-polycaprolactone diol, ou un mélange de ceux-ci.

13. Méthode selon l'une quelconque des revendications précédentes dans laquelle le composant prépolymère et/ou le composant de polymérisation inclut une charge.

14. Méthode selon l'une quelconque des revendications précédentes, dans laquelle la polyamine primaire dans le composant de polymérisation est une amine aliphatique en C₁₋₁₄.

15. Méthode selon la revendication 14, dans laquelle ladite polyamine primaire est une éthylène diamine.

16. Méthode selon l'une quelconque des revendications précédentes dans laquelle 1 à 5 parties en poids de la polyamine primaire est présente pour 100 parties de polyol de polymérisation dans le composant de polymérisation.

17. Méthode selon l'une quelconque des revendications précédentes dans laquelle le composant de polymérisation (b) inclut un catalyseur pour la réaction de formation d'uréthane.

18. Procédé comprenant l'adhésion de deux articles ensemble en utilisant un adhésif à base d'uréthane à deux composants selon l'une quelconque des revendications 1 à 17.

19. Procédé selon la revendication 18, dans lequel une ou les deux surfaces des articles est exempte de traitement pour l'adhésion.

20. Procédé selon la revendication 18, ou la revendication 19, dans lequel un ou les deux articles est constitué de plastique renforcé par des libres.

21. Procédé selon l'une quelconque des revendications 18 à 20, dans lequel l'adhésif est polymérisé par chauffage au-dessus de 50°C.

22. Composite collé obtenu par un procédé selon l'une quelconque des revendications 18 à 21.